CN205990231U - The producing and burner of aqueous medium fuel - Google Patents
The producing and burner of aqueous medium fuel Download PDFInfo
- Publication number
- CN205990231U CN205990231U CN201620874888.6U CN201620874888U CN205990231U CN 205990231 U CN205990231 U CN 205990231U CN 201620874888 U CN201620874888 U CN 201620874888U CN 205990231 U CN205990231 U CN 205990231U
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- CN
- China
- Prior art keywords
- burner
- catalysis
- cover plate
- tubular pole
- catalysis electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Abstract
The producing and burner of a kind of aqueous medium fuel, it is related to burner apparatus, including pressure pump, pressurized tank, burner and electrostatic generator, the outlet of pressure pump is attached by the bottom of check-valves and pressurized tank, burner assembly is by catalysis electrode, tubular pole seat and cover plate composition, there is water guide duct in the body of catalysis electrode, many catalysis electrodes are arranged on the screw socket of tubular pole seat, water guide duct in catalysis electrode body is connected with space in the pipe of tubular pole seat, in the pipe of tubular pole seat, space constitutes pressure-bearing hydroecium, cover plate is arranged on the body of tubular pole seat by insulated support, the micropore cone of catalysis electrode upper semisection is placed among the duct of cover plate；Catalysis electrode is electrically connected with the anode interface of electrostatic generator, and cover plate is electrically connected with the negative pole interface of electrostatic generator.This utility model, with aqueous medium as gasified raw material, passes through pressure permeation, catalysis and ionization water, and the vaporising fuel being decomposed into hydrogen-oxygen is burnt.
Description
Technical field
This utility model is related to burner apparatus, especially relates to a kind of aqueous medium combustion apparatus.
Background technology
Water is a kind of material the abundantest containing protium, and each hydrone is by two hydrogen atoms and an oxygen atom knot
Conjunction forms, and containing the hydrogen more than 111 kilograms in every cubic meter of water, its quality capacity is more than 11.1%, and the calorific capacity of hydrogen is high, combustion
Burn the heat that 1 kg hydrogen can release 142120kj, be three times of gasoline.Water is developed into a kind of energy to apply, during burning
Do not produce carbon dioxide, product only has water, can be repeatedly circulated, to improving air acid rain environment, reduce dioxy in air
Change carbon content, thus mitigating greenhouse effect have great benefit.Therefore, exploitation aqueous medium fuel not only can solve energy shortage
Situation, and environment protecting project.However, the hydrogen atom in hydrone and oxygen atom combine to obtain very firm, high-temperature heating
Method need to be heated to more than 3000 DEG C hydrone and be decomposed, the so high temperature of general mode of heating difficult to reach；Industry
On with current method decompose hydrone hydrogen manufacturing, decomposition rate is slow, efficiency is low, and consume energy very big.
Utility model content
The purpose of this utility model is intended to overcome existing pyrolysis water hydrogen manufacturing and current method to decompose the shortcoming of hydrone hydrogen manufacturing, carries
For a kind of producing and burner of aqueous medium fuel, water is applied as a kind of energy, to realize cleaning burning, protecting ecology
Environment.
The producing and burner, including pressure pump, pressurized tank, burner of a kind of aqueous medium fuel of the present utility model
And electrostatic generator, the outlet of pressure pump is attached by the bottom of check-valves and pressurized tank, it is characterized in that burner
Assembly 1 is made up of catalysis electrode 1-4, tubular pole seat 1-7 and cover plate 1-1, and wherein, catalysis electrode 1-4 is more than one, catalysis
The upper semisection of electrode 1-4 is micropore conical structure, has water guide duct 1-401 in the lower half segment body of catalysis electrode 1-4；Tubular type electricity
Electrode seat 1-7 is the hollow circular-tube structure of endcapped, has a row for installing the screw socket of catalysis electrode on tubular pole seat 1-7
1-3；Duct 1-2 with catalysis electrode equal number is had on cover plate 1-1；Many catalysis electrode 1-4 are arranged on tubular pole seat 1-7
Screw socket 1-3 on, the water guide duct 1-401 in catalysis electrode 1-4 body is connected with space in the pipe of tubular pole seat 1-7, pipe
The front end of formula electrode tip holder 1-7 has water supply connector 21 to access, and in the pipe of tubular pole seat 1-7, space constitutes pressure-bearing hydroecium 20；Cover plate
1-1 is arranged on the body of tubular pole seat 1-7 by insulated support 1-6, the micropore cone of catalysis electrode 1-4 upper semisection
It is placed among the duct 1-2 of cover plate 1-1；Catalysis electrode 1-4 passes through metal wall and the electrostatic generator of tubular pole seat 1-7
Anode interface is electrically connected, and cover plate 1-1 is electrically connected with the negative pole interface of electrostatic generator；Tubular pole seat 1-7
On water supply connector 21 be connected on the pipeline between check-valves 12 and pressurized tank 16.
In this utility model, catalysis electrode 1-4 is metal powder sintered microporous filter membrane structure, and catalysis electrode 1-4 is constituted
Hydrone filters and catalysis element, and when being embodied as, catalysis electrode 1-4 is the material burning of tungsten powder and the mixing of nickel-sulfur alloy powder
Form tungsten nickel pseudo-alloy part, when firing, the neither mutual phased soln of tungsten, nickel-sulfur alloy, also do not form intermetallic compound, formed
Pseudo-alloy be organized as two phase structures of tungsten particle, nickel-sulfur alloy granule, there is micro-pore, micro-pore in pseudo-alloy tissue
Constitute the filtration channel of hydrone, there is the effect filtering hydrone, nickel-sulfur alloy therein has to the decomposition of hydrone urges
Change acts on, and makes hydrone be easier to decompose；There are space, catalysis electricity between the duct 1-2 wall body of catalysis electrode 1-4 and cover plate 1-1
Space between the duct 1-2 wall body of pole 1-4 and cover plate 1-1 constitutes electrostatic field；There is normally closed row in the tail end of tubular pole seat 1-7
Air valve 2, normally closed air bleeding valve 2 is communicated to space in the pipe of tubular pole seat 1-7；Duct 1-2 on cover plate 1-1 is up-small and down-big
Inverted tubaeform structure；Breathing interface 16-1 is arranged at the bottom of pressurized tank, and the outlet of pressure pump passes through check-valves 12 and pressurized tank
The breathing interface 16-1 of bottom is attached；The pipeline that pressure pump 8 accesses there is filter 10；Burner assembly 1 is one
More than individual, when burner assembly 1 is multiple, the pipe interface between check-valves 12 and pressurized tank 16 is connected to by water knockout drum
In the water supply connector of each burner assembly, the catalysis electrode of each burner assembly is connect with the positive pole of parallel way and electrostatic generator
Mouth is electrically connected, and the cover plate of each burner assembly is electrically connected with the negative pole interface of parallel way and electrostatic generator
Connect.
This utility model is suitable for application on Industrial Boiler, with aqueous medium as gasified raw material, realizes cleaning burning, obtains heat
Can, during application, pressure pump, pressurized tank, electrostatic generator and burner assembly 1 are arranged in respective frame.During work, right
Apply more than 10,000 volts of electrostatic between catalysis electrode 1-4 and cover plate 1-1, make at the micropore cone of catalysis electrode 1-4 upper semisection
In the electrostatic field among the 1-2 of duct, to increase the catalysis activity of catalysis electrode 1-4, and ionization is formed to hydrone；
Using pure water as raw water, the pressurized water pump of raw water 8 enters in the pressure-bearing hydroecium 20 of burner assembly 1, simultaneously former
Material water is entered in pressurized tank by the breathing interface 16-1 of pressurized tank 16 bottom, so that the upper air in pressurized tank 16 is compressed,
Form compressed air, the water of pressurized tank 16 bottom has pressure in the presence of compressed air, the hydraulic pressure in pressure-bearing hydroecium 20 with
The hydraulic pressure of pressurized tank 16 bottom is equal.The pure water in pressure-bearing hydroecium 20 with pressure is penetrated into by water guide duct 1-401 and urges
In the micro-pore of polarizing electrode 1-4, the micro-pore of catalysis electrode 1-4 filters to hydrone, makes macromolecular mass become little
Molecule, the activity of hydrone is improved, and makes hydrone be easier to be decomposed, meanwhile, the nickel-sulfur alloy material of catalysis electrode 1-4
Material carries out catalytic decomposition to hydrone.Hydrone, through pressure permeation, is changed into small molecular cluster structure by macromolecular mass, then warp
The catalysis of nickel-sulfur alloy material and electrostatic FI, are decomposed into hydrogen, oxygen and active hydrogen atom, active oxygen atom, reactive hydrogen
The activity chemistry thing of oxygen atomic group, escapes from the micropore cone of catalysis electrode 1-4 upper semisection, becomes vaporising fuel, enters
To in the 1-2 of duct, the vaporising fuel of hydrone conversion is entered by the high-voltage spark between catalysis electrode 1-4 and duct 1-2 wall body
Row is lighted, and carries out back reaction burning, releases heat energy.In said process, the water in pressure-bearing hydroecium 20 is with infiltration catalysis electrode 1-4's
Water produces cooling effect to catalysis electrode 1-4, protects catalysis electrode 1-4 not to be burned.This utility model to be improved using electrostatic
The catalysis activity of catalysis electrode 1-4 and ionize hydrone using electrostatic field, reduces the temperature requirement of pyrolysis hydrone, is consumed
Electric energy is few, and the decomposition efficiency of hydrone is high.
The beneficial effects of the utility model are：Producing and burner of the aqueous medium fuel providing, is suitable in industrial pot
Apply on stove, with aqueous medium as gasified raw material, hydrone is passed through pressure permeation, small molecule unity is changed into by macromolecular mass
Structure, then through the catalysis of nickel-sulfur alloy material and electrostatic FI, the vaporising fuel being decomposed into hydrogen-oxygen is burnt, using water as one kind
The energy, to apply, is realized cleaning burning, is preserved the ecological environment.
Brief description
Fig. 1 is producing and burner structure chart of aqueous medium fuel of the present utility model.
Fig. 2 is the enlarged drawing of catalysis electrode of the present utility model.
In figure：1. burner assembly, 1-1. cover plate, 1-2. duct, 1-3. screw socket, 1-4. catalysis electrode, 1-401. water guide
Duct, 1-402. external screw thread, 1-403. outer-hexagonal body, 1-404. micropore cone, 1-5. Positioning screw, 1-6. insulating supporting
Part, 1-7. tubular pole seat, 1-8. water inlet interface, 2. normally closed air bleeding valve, 3. return line, 4. insulating support, 5. high-voltage line, 6. quiet
Electric generator, 6-1. negative pole interface, 6-2. anode interface, 7. penstocks, 8. pressure pump, 9. communicating pipe, 10. filter,
11. feed pipes, 12. check-valves, 13. threeways, 14. frames, 15. pressure pure water, 16. pressurized tanks, 16-1. breathes interface, 16-
2. satellite interface, 16-3. overhauls evacuated tube, 17. compressed airs, 18. pressure controllers, 19. maintenance exhaust-valves, 20. artesian waters
Room, 21. water supply connectors.
Specific embodiment
In embodiment shown in embodiment 1 Fig. 1, aqueous medium fuel produce and burner is mainly by pressure pump
8th, pressurized tank 16, burner assembly 1 and electrostatic generator 6 form, and the outlet of pressure pump 8 passes through check-valves 12 and pressurized tank
The breathing interface 16-1 of bottom is attached, and burner assembly 1 includes catalysis electrode 1-4, tubular pole seat 1-7 and cover plate 1-1,
Wherein, catalysis electrode 1-4 is more than one, and the upper semisection of catalysis electrode 1-4 is micropore conical structure, catalysis electrode 1-4's
There is water guide duct 1-401 in lower half segment body；Tubular pole seat 1-7 is the hollow circular-tube structure of endcapped, in tubular pole seat
One row is had on 1-7 for installing the screw socket 1-3 of catalysis electrode；Duct 1-2 with catalysis electrode equal number is had on cover plate 1-1；
Many catalysis electrode 1-4 are arranged on the screw socket 1-3 of tubular pole seat 1-7, the water guide duct 1-401 in catalysis electrode 1-4 body
Connect with space in the pipe of tubular pole seat 1-7, have water supply connector 21 to access in the front end of tubular pole seat 1-7, tubular pole
In the pipe of seat 1-7, space constitutes pressure-bearing hydroecium 20；Cover plate 1-1 is arranged on the pipe of tubular pole seat 1-7 by insulated support 1-6
On body, the micropore cone of catalysis electrode 1-4 upper semisection is placed among the duct 1-2 of cover plate 1-1, catalysis electrode 1-4 and duct
There is space between 1-2 wall body；Catalysis electrode 1-4 is connect with the positive pole of electrostatic generator by the metal wall of tubular pole seat 1-7
Mouth is electrically connected, and cover plate 1-1 is electrically connected with the negative pole interface of electrostatic generator, catalysis electrode 1-4 and cover plate 1-1
Duct 1-2 wall body between space constitute electrostatic field；Water supply connector 21 on tubular pole seat 1-7 be connected to check-valves 12 with
On pipeline between pressurized tank 16.In the present embodiment, catalysis electrode 1-4 is metal powder sintered microporous filter membrane structure, catalysis
Electrode 1-4 constitutes hydrone and filters and catalysis element, and catalysis electrode 1-4 is the material burning of tungsten powder and the mixing of nickel-sulfur alloy powder
Form tungsten nickel pseudo-alloy part, when firing, the neither mutual phased soln of tungsten, nickel-sulfur alloy, also do not form intermetallic compound, formed
Pseudo-alloy be organized as two phase structures of tungsten particle, nickel-sulfur alloy granule, there is micro-pore, micro-pore in pseudo-alloy tissue
Constitute the filtration channel of hydrone, there is the effect filtering hydrone, nickel-sulfur alloy therein has to the decomposition of hydrone urges
Change acts on, and makes hydrone be easier to decompose；There is normally closed air bleeding valve 2 in the tail end of tubular pole seat 1-7, normally closed air bleeding valve 2 connects
The space in the pipe of tubular pole seat 1-7, when using for the first time, opens normally closed air bleeding valve 2, the air in pressure-bearing hydroecium 20 is with water inlet
And discharge, it is easy into water to make；Duct 1-2 on cover plate 1-1 is up-small and down-big inverted tubaeform structure；Access in pressure pump 8
Pipeline on have filter 10；There are pressure controller 18 and maintenance exhaust-valve 19 on the top of pressurized tank 16 or top.
The present embodiment uses in Industrial Boiler, and burner assembly 1 is arranged on the insulating support 4 in industrial boiler furnace
On, cover plate 1-1 is carried out with ground protection process, pressure pump 8, pressurized tank 16 and electrostatic generator 6 are arranged on Industrial Boiler
Periphery.During work, to the electrostatic applying more than 10,000 volts between catalysis electrode 1-4 and cover plate 1-1, make catalysis electrode 1-4 upper semisection
Micropore cone be in the electrostatic field among the 1-2 of duct, to increase the catalysis activity of catalysis electrode 1-4, and to moisture
Son forms ionization；Using pure water as raw water, the pressurized water pump of raw water 8 enters into the pressure-bearing of burner assembly 1
In hydroecium 20, raw water is entered in pressurized tank by the breathing interface 16-1 of pressurized tank 16 bottom simultaneously, makes upper in pressurized tank 16
Portion's air is compressed, and forms compressed air, and the water of pressurized tank 16 bottom has pressure, artesian water in the presence of compressed air
Hydraulic pressure in room 20 is equal with the hydraulic pressure of pressurized tank 16 bottom.The pure water in pressure-bearing hydroecium 20 with pressure passes through water guide duct
1-401 penetrates in the micro-pore of catalysis electrode 1-4, and the micro-pore of catalysis electrode 1-4 filters to hydrone, makes big
Micel becomes small molecule, and the activity of hydrone is improved, and makes hydrone be easier to be decomposed, meanwhile, catalysis electrode 1-4
Nickel-sulfur alloy material catalytic decomposition is carried out to hydrone.Hydrone, through pressure permeation, is changed into little point by macromolecular mass
Sub- unity structure, then through the catalysis of nickel-sulfur alloy material and electrostatic FI, it is decomposed into hydrogen, oxygen and active hydrogen atom, activity
Oxygen atom, the activity chemistry thing of reactive hydrogen oxygen atomic group, escape from the micropore cone of catalysis electrode 1-4 upper semisection, become
Vaporising fuel, enters in the 1-2 of duct, and the vaporising fuel of hydrone conversion is by between catalysis electrode 1-4 and duct 1-2 wall body
High-voltage spark is lighted, and carries out back reaction burning, releases heat energy.Operation pressure in above-mentioned work process, in pressurized tank 16
Power is controlled by pressure controller 18, and when the pressure in pressurized tank 16 is less than the threshold pression setting, pressure controller 18 connects
The power supply of logical pressure pump 8, makes pressure pump 8 run, and carries out moisturizing to pressurized tank 16, so that air in pressurized tank 16 is compressed and
Pressure inside the tank is made to raise；When the pressure in pressurized tank 16 reaches the pressure upper limit of setting, pressure controller 18 disconnects pressure (hydraulic) water
The power supply of pump 8, makes pressure pump 8 stop, and by the control of pressure controller 18, makes the pressure in pressurized tank 16 in the model setting
Enclose interior holding constant.
Embodiment 2 aqueous medium fuel produce and burner mainly by pressure pump 8, pressurized tank 16, electrostatic occur
Device 6 and three burner assembly compositions, the pipe interface between check-valves 12 and pressurized tank 16 is connected to three by water knockout drum
In the water supply connector of burner assembly, the catalysis electrode of three burner assemblies is connect with the positive pole of parallel way and electrostatic generator
Mouth is electrically connected, and the cover plate of each burner assembly is electrically connected with the negative pole interface of parallel way and electrostatic generator
Connect.Other structures are basically the same as those in the first embodiment, and repeat no more.
Claims (8)
1. the producing and burner of a kind of aqueous medium fuel, including pressure pump, pressurized tank, burner and electrostatic generator,
The outlet of pressure pump is attached by the bottom of check-valves and pressurized tank, it is characterized in that burner assembly（1）By being catalyzed
Electrode（1-4）, tubular pole seat（1-7）And cover plate（1-1）Composition, wherein, catalysis electrode（1-4）For more than one, catalysis electricity
Pole（1-4）Upper semisection be micropore conical structure, catalysis electrode（1-4）Lower half segment body in have water guide duct（1-401）；Pipe
Formula electrode tip holder（1-7）For the hollow circular-tube structure of endcapped, in tubular pole seat（1-7）On have a row for install catalysis electric
The screw socket of pole（1-3）；Cover plate（1-1）On have duct with catalysis electrode equal number（1-2）；Many catalysis electrodes（1-4）Peace
It is contained in tubular pole seat（1-7）Screw socket（1-3）On, catalysis electrode（1-4）Water guide duct in body（1-401）With tubular pole
Seat（1-7）Pipe in space connection, in tubular pole seat（1-7）Front end have water supply connector（21）Access, tubular pole seat（1-
7）Pipe in space constitute pressure-bearing hydroecium（20）；Cover plate（1-1）By insulated support（1-6）It is arranged on tubular pole seat（1-
7）Body on, catalysis electrode（1-4）The micropore cone of upper semisection is placed in cover plate（1-1）Duct（1-2）Among；Catalysis electricity
Pole（1-4）By tubular pole seat（1-7）Metal wall be electrically connected with the anode interface of electrostatic generator, cover plate
（1-1）It is electrically connected with the negative pole interface of electrostatic generator；Tubular pole seat（1-7）On water supply connector（21）It is connected to
Check-valves（12）With pressurized tank（16）Between pipeline on.
2. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that catalysis electrode（1-4）
For metal powder sintered microporous filter membrane structure, catalysis electrode（1-4）Constitute hydrone to filter and catalysis element.
3. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that catalysis electrode（1-4）
With cover plate（1-1）Duct（1-2）There are space, catalysis electrode between wall body（1-4）With cover plate（1-1）Duct（1-2）Wall body
Between space constitute electrostatic field.
4. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that in tubular pole seat
（1-7）Tail end have normally closed air bleeding valve（2）, normally closed air bleeding valve（2）It is communicated to tubular pole seat（1-7）Pipe in space.
5. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that cover plate（1-1）On
Duct（1-2）For up-small and down-big inverted tubaeform structure.
6. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that the bottom of pressurized tank
There is breathing interface（16-1）, the outlet of pressure pump passes through the breathing interface of check-valves 12 and pressure pot bottom（16-1）Carry out
Connect.
7. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that in pressure pump（8）
There is filter on the pipeline accessing（10）.
8. the producing and burner of a kind of aqueous medium fuel according to claim 1, is characterized in that burner assembly（1）
For more than one, work as burner assembly（1）For multiple when, check-valves（12）With pressurized tank（16）Between pipe interface pass through point
Hydrophone is connected in the water supply connector of each burner assembly, and the catalysis electrode of each burner assembly is occurred with electrostatic with parallel way
The anode interface of device is electrically connected, and the cover plate of each burner assembly is entered with the negative pole interface of parallel way and electrostatic generator
Row electrical connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620874888.6U CN205990231U (en) | 2016-08-15 | 2016-08-15 | The producing and burner of aqueous medium fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620874888.6U CN205990231U (en) | 2016-08-15 | 2016-08-15 | The producing and burner of aqueous medium fuel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205990231U true CN205990231U (en) | 2017-03-01 |
Family
ID=58107342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620874888.6U Withdrawn - After Issue CN205990231U (en) | 2016-08-15 | 2016-08-15 | The producing and burner of aqueous medium fuel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205990231U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082123A (en) * | 2016-08-15 | 2016-11-09 | 衢州昀睿工业设计有限公司 | Producing and burner of aqueous medium fuel |
-
2016
- 2016-08-15 CN CN201620874888.6U patent/CN205990231U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082123A (en) * | 2016-08-15 | 2016-11-09 | 衢州昀睿工业设计有限公司 | Producing and burner of aqueous medium fuel |
| CN106082123B (en) * | 2016-08-15 | 2018-04-03 | 衢州昀睿工业设计有限公司 | Aqueous medium fuel produce and burner |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170301 Effective date of abandoning: 20180403 |
|
| AV01 | Patent right actively abandoned |